Role of Operating Conditions in a Pilot Scale Investigation of Hollow Fiber Forward Osmosis Membrane Modules.

aquaporin forward osmosis hollow fiber thin film composite

Journal

Membranes
ISSN: 2077-0375
Titre abrégé: Membranes (Basel)
Pays: Switzerland
ID NLM: 101577807

Informations de publication

Date de publication:
03 Jun 2019
Historique:
received: 29 04 2019
revised: 29 05 2019
accepted: 29 05 2019
entrez: 6 6 2019
pubmed: 6 6 2019
medline: 6 6 2019
Statut: epublish

Résumé

Although forward osmosis (FO) membranes have shown great promise for many applications, there are few studies attempting to create a systematization of the testing conditions at a pilot scale for FO membrane modules. To address this issue, hollow fiber forward osmosis (HFFO) membrane modules with different performances (water flux and solute rejection) have been investigated at different operating conditions. Various draw and feed flow rates, draw solute types and concentrations, transmembrane pressures, temperatures, and operation modes have been studied using two model feed solutions-deionized water and artificial seawater. The significance of the operational conditions in the FO process was attributed to a dominant role of concentration polarization (CP) effects, where the selected draw solute and draw concentration had the biggest impact on membrane performance due to internal CP. Additionally, the rejection of the HFFO membranes using three model solutes (caffeine, niacin, and urea) were determined under both FO and reverse osmosis (RO) conditions with the same process recovery. FO rejections had an increase of 2% for caffeine, 19% for niacin, and 740% for urea compared to the RO rejections. Overall, this is the first extensive study of commercially available inside-out HFFO membrane modules.

Identifiants

pubmed: 31163624
pii: membranes9060066
doi: 10.3390/membranes9060066
pmc: PMC6631378
pii:
doi:

Types de publication

Journal Article

Langues

eng

Subventions

Organisme : Innovationsfonden
ID : 8053-00027B

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Auteurs

Victoria Sanahuja-Embuena (V)

Department of Environmental Engineering, Technical University of Denmark, Miløvej 113, 2800 Kongens Lyngby, Denmark. vics@env.dtu.dk.
Aquaporin A/S, Nymøllevej 78, 2800 Kongens Lyngby, Denmark. vics@env.dtu.dk.

Gabriel Khensir (G)

Department of Chemical and Biochemical Engineering, Technical University of Denmark, Søltofts Plads, 2800 Kongens Lyngby, Denmark. gabiih@live.dk.

Mohamed Yusuf (M)

Department of Chemical and Biochemical Engineering, Technical University of Denmark, Søltofts Plads, 2800 Kongens Lyngby, Denmark. Moe0207@hotmail.com.

Mads Friis Andersen (MF)

Aquaporin A/S, Nymøllevej 78, 2800 Kongens Lyngby, Denmark. mfr@aquaporin.com.

Xuan Tung Nguyen (XT)

Aquaporin A/S, Nymøllevej 78, 2800 Kongens Lyngby, Denmark. xtn@aquaporin.com.

Krzysztof Trzaskus (K)

Aquaporin A/S, Nymøllevej 78, 2800 Kongens Lyngby, Denmark. ktr@aquaporin.com.

Manuel Pinelo (M)

Department of Chemical and Biochemical Engineering, Technical University of Denmark, Søltofts Plads, 2800 Kongens Lyngby, Denmark. mp@kt.dtu.dk.

Claus Helix-Nielsen (C)

Department of Environmental Engineering, Technical University of Denmark, Miløvej 113, 2800 Kongens Lyngby, Denmark. clhe@env.dtu.dk.

Classifications MeSH